Study of Selected Factors Influencing Carbon Dioxide Separation from Simulated Biogas by Hydrate Formation

被引:17
|
作者
Yue, Gang [1 ,3 ]
Liu, Ai-xian [1 ,2 ]
Sun, Qiang [1 ,3 ]
Li, Xing-xun [1 ,3 ]
Lan, Wen-jie [1 ,3 ]
Yang, Lan-ying [1 ,3 ]
Guo, Xu-qiang [1 ,2 ]
机构
[1] China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
[2] China Univ Petr Beijing Karamay, Karamay 834400, Peoples R China
[3] China Univ Petr, Beijing 102249, Peoples R China
来源
关键词
NATURAL-GAS; CO2; REMOVAL; PHASE-EQUILIBRIUM; IONIC LIQUIDS; ENERGY-SOURCE; BROMIDE; DISSOCIATION; CAPTURE; CRYSTALLIZATION; SURFACTANTS;
D O I
10.1021/acs.jced.8b00567
中图分类号
O414.1 [热力学];
学科分类号
摘要
CH4 concentration and CO2 separation from biogas (CH4/CO2) by an one-stage hydrate formation was supposed to be a prospective and economical practicable technology compared with traditional gas separation methods. We investigated the influence of 1-butyl-3-methylimidazolium hexafluorophosphate ([BMIM] PF6) on simulated biogas (64.0 mol %CH4/CO2) hydrate separation in this work. The thermodynamic promoter TBAB was combined with [BMIM] PF6 to investigate binary gas hydrate formation and separation efficiency. Different parameters which affected hydrate formation were investigated. The concentration of [BMIM] PF6 was 1000/2000/3000 ppm, and the optimized concentration of TBAB was 4 wt %. With respect to the hydrate gas separation results, the addition of TBAB can decrease CH4/CO2 hydrate formation pressure greatly and the hydrate formation induction time. CH4 in the remaining gas can be increased from 64.0 to 79.90 mol %, and CH4 recovery can arrive at 95.83%. Meanwhile, the addition of [BMIM] PF6 could increase the CO2 mole friction in hydrate from 36.0 to 58.63 mol %. So it was demonstrated that the combination of TBAB + [BMIM] PF6 would have a great application prospect on biogas purification technology.
引用
收藏
页码:3941 / 3955
页数:15
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